US5032324A - High yield air diffuser for tanks used in the aerobic treatment of waste waters - Google Patents

High yield air diffuser for tanks used in the aerobic treatment of waste waters Download PDF

Info

Publication number
US5032324A
US5032324A US07/350,528 US35052889A US5032324A US 5032324 A US5032324 A US 5032324A US 35052889 A US35052889 A US 35052889A US 5032324 A US5032324 A US 5032324A
Authority
US
United States
Prior art keywords
diffuser
distributor
base
frusto
cylindrical body
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
US07/350,528
Inventor
Giacinto Petrillo
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Application granted granted Critical
Publication of US5032324A publication Critical patent/US5032324A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/1278—Provisions for mixing or aeration of the mixed liquor
    • C02F3/1284—Mixing devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B01F23/23231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
    • B01F23/232311—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit the conduits being vertical draft pipes with a lower intake end and an upper exit end
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30—Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32—Driving arrangements
    • B01F35/32005—Type of drive
    • B01F35/3203—Gas driven
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/20—Activated sludge processes using diffusers
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/22—Activated sludge processes using circulation pipes
    • C02F3/223—Activated sludge processes using circulation pipes using "air-lift"
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30—Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32—Driving arrangements
    • B01F35/32005—Type of drive
    • B01F35/32015—Flow driven
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

Definitions

  • the present invention refers to the diffusers used in tanks for the aerobic purification of waste waters.
  • the known diffusers are made in such a way so as to disperse the air blown into pipes running across the bottom of tanks for aerobic treatment filled with waste waters.
  • Said diffusers are located at each air exit from the above mentioned pipes. These diffusers have however a reduced efficiency because the air is distributed in bubbles having a dimension that is unsuitable for obtaining a uniform dispersion and efficient transfer of the oxygen to the liquid; in fact, the bubbles having big dimensions reach the surface before an effective oxygen transfer to the waters to be treated takes place.
  • U.S. Pat. No. 3,852,384 foresees that the blown-in air bubbles be forced to follow a not rectilinear path, in particular a spiral path, that increases the bubbles stay time in the waters to be treated.
  • the spiral path is obtained by collecting the blown-in air in vertical cylindrical elements where one or more helical baffles are provided so as to act as guides for the bubbles. In this way the air and water mixture follows a spiral path that prolongs the interface contact between bubbles and liquid.
  • the aforesaid cylindrical elements are placed above the pipes running horizontally, near the bottom of the tank, these pipes being horizontal and perforated in the lower part for the passage of the blown-in air. Nevertheless, the yield has not reached optimum levels.
  • the object of the present invention is that of improving the yield of the diffusers so as to obtain finely dispersed bubbles creating an efficacious transfer of the oxygen to the waters to be treated.
  • the sparger, or dispersing means consists of a hopper having the major base provided with tongues that radially depart from its periphery in order to catch the bubbles coming out from a horizontal pipe running near the bottom of the tank and to cut the mass of bubbles creating an additional turbulence.
  • the minor base of the sparger is provided with an edge protruding towards the outside and openings for the passage of tie rods for the anchorage of the diffuser.
  • the minor base is circumferentially provided with a seat for receiving the end of the cylindrical body which is preferably formed by a plurality of sections welded together.
  • the distributor placed at the top of the cylindrical element comprises a truncated cone shaped portion with the major base open and the minor base provided with openings radially distributed. Moreover, the lateral surface is provided with further slots for the outlet of bubbles.
  • the minor base consists of a tapered element with the apex of the cone turned towards the inside of the diffuser.
  • the distributor is fixed to the cylindrical body by means of another hopper quite similar to the one of the sparger, with the major base facing upwards so that this hopper is capable of helping the discharge of the air-water mixture.
  • the described diffusers are uniformly distributed at the bottom of the tank and anchored to supports, in the shape of concrete blocks, preferably by means of tie rods fixed with bolts screwed on threaded rods protruding from the concrete blocks, a perforated plate that is inserted on the aforesaid rods being foreseen at the lower end of the tie rod.
  • the tie rods are fixed on the protruding edge of the second sparger that surrounds the distributor, preferably with nuts screwn on their threaded ends by interposing suitable washers.
  • FIG. 1 shows a partially sectioned side view of the diffuser anchored at its support
  • FIG. 2 shows a side view of the sparger
  • FIG. 3 shows a view of the sparger taken along line 3--3 of FIG. 2;
  • FIG. 4 shows a view of the sparger taken along line 4--4 of FIG. 2;
  • FIG. 5 shows a partially sectioned side view of the distributor
  • FIG. 6 shows an upper view of the distributor
  • FIG. 7 shows a detail of the sparger
  • FIG. 8 shows a section of the tank with the diffusers installed.
  • a diffuser 10 is shown in FIG. 1 comprising a cylindrical body 11 containing two helical sections 12 and 12a that cross each other, forming two spiral canals for discharging the air-water mixture to be treated.
  • the cylindrical body 11 is preferably made of a plurality of sections 11a.
  • the diffuser is provided at its base with a sparger, or dispersing means 13 and at the top with a distributor 14 which is held on the end of the diffuser by means of a second sparger 13a, the hopper 15 of which laterally surrounds said distributor 14.
  • the sparger 13 (that is quite similar to sparger 13a) is shown in detail in FIGS. 2, 3 and 4. It is made of a hopper 15, the minor base of which has a periphery 17 provided with tongues 16 perpendicular to said periphery 17. The minor base is also provided with a protruding edge 18 having openings 19 for the passage of tie rods 21 (FIG. 1) fixing the diffuser 10.
  • the side surface of the hopper (15) has further openings 20 so as to allow the fixing tie rods 21 to extend perpendicular to support 22 on which they are fixed.
  • This protruding edge 18 also has reinforcements 23 circumferentially disposed.
  • the minor base of hopper 15 is provided circumferentially with a seat 28 capable of receiving an end of the cylindrical body 11.
  • Distributor 14 is shown in FIGS. 5 and 6. It comprises a truncated cone shaped portion 24, the minor base of which consists in a tapered element 25 having the apex of the cone turned towards the inside of portion 24. It can be noticed that the tapered element is provided with openings 26, having almost trapezoidal shape. Furthermore, the truncated cone shaped portion 24 is also laterally provided with rectangular openings 27. These openings 26 and 27 are used for the distribution of the mixture of air-water to be treated.
  • Said truncated cone portion 24 is held at the end of the cylindrical body 11 by means of a second sparger 13a over-turned with respect to the position of sparger 13 (see FIG. 1).
  • An engaging means 29 is foreseen inserted in seat 28 of the minor base of the hopper 15, placed along the major base of the truncated cone portion 24.
  • FIG. 7 A detail of the protruding edge 18 is shown in FIG. 7; the reinforcements 23 and the openings 19 for the passage of tie rods 21 are clearly visible.
  • FIG. 8 shows a transverse section of a tank used for the aerobic treatment of waste waters; in said tank the diffusers 10 are placed and kept in their position on supports 22 in the shape of concrete blocks. The diffusers are placed on top of conduits 35 for the blown-in air, that run horizontally near the bottom of the tank, these conduits 35 also being anchored to support 22 and provided in the lower part with openings for the air distribution.
  • FIG. 1 shows a perforated fastening system in detail, however it is obvious that other systems can be used.
  • Tie rods 21 have at the lower end a perforated plate 32 inserted on the threaded rods 30 protruding from support 22, the perforated plate being held in place by a nut 31 and washers.
  • the tie rods are fixed at the top to the protruding edge 18 of the sparger 13a by means of nuts screwed on their threaded ends extending from apertures 19.
  • the diffuser The function of the diffuser is as follows: the air bubbles delivered from conduit 35 are caught and divided by means of the lower sparger 13, thus they enter the cylindrical body 11 where they follow a spiral path mixing and interact with the liquid to be treated, finally they reach distributor 14 and exit finely divided.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

Diffuser (10) comprising a cylindrical body (11) inside which a helical section (12, 12a) is provided. At the base and at the top, a sparger (13) and a distributor (14) respectively are foreseen. Preferably a second sparger is foreseen at the top, around the distributor (14). Each sparger (13, 13a) consists of a hopper (15) having the major base provided with tongues (16) that radially depart from its periphery. Distributor (14) comprises a truncated-cone portion (24) having the minor base made up of a conical element (25), openings (26, 27) being provided both in the conical element and in the lateral surface of the hopper (15). The diffuser (10) is fixed to a suitable support (22) by means of tie rods (21) held on the protruding edge (18) of the upper sparger (13a).

Description

The present invention refers to the diffusers used in tanks for the aerobic purification of waste waters.
The known diffusers are made in such a way so as to disperse the air blown into pipes running across the bottom of tanks for aerobic treatment filled with waste waters.
Said diffusers are located at each air exit from the above mentioned pipes. These diffusers have however a reduced efficiency because the air is distributed in bubbles having a dimension that is unsuitable for obtaining a uniform dispersion and efficient transfer of the oxygen to the liquid; in fact, the bubbles having big dimensions reach the surface before an effective oxygen transfer to the waters to be treated takes place.
In order to improve the efficiency of the diffusers, U.S. Pat. No. 3,852,384 foresees that the blown-in air bubbles be forced to follow a not rectilinear path, in particular a spiral path, that increases the bubbles stay time in the waters to be treated. The spiral path is obtained by collecting the blown-in air in vertical cylindrical elements where one or more helical baffles are provided so as to act as guides for the bubbles. In this way the air and water mixture follows a spiral path that prolongs the interface contact between bubbles and liquid. The aforesaid cylindrical elements are placed above the pipes running horizontally, near the bottom of the tank, these pipes being horizontal and perforated in the lower part for the passage of the blown-in air. Nevertheless, the yield has not reached optimum levels.
The object of the present invention is that of improving the yield of the diffusers so as to obtain finely dispersed bubbles creating an efficacious transfer of the oxygen to the waters to be treated.
This aim is achieved by providing at the base and top of the cylindrical body, comprising at its interior one or more helical sections, a sparger and a distributor respectively. The sparger, or dispersing means consists of a hopper having the major base provided with tongues that radially depart from its periphery in order to catch the bubbles coming out from a horizontal pipe running near the bottom of the tank and to cut the mass of bubbles creating an additional turbulence. The minor base of the sparger is provided with an edge protruding towards the outside and openings for the passage of tie rods for the anchorage of the diffuser.
The minor base is circumferentially provided with a seat for receiving the end of the cylindrical body which is preferably formed by a plurality of sections welded together.
The distributor placed at the top of the cylindrical element comprises a truncated cone shaped portion with the major base open and the minor base provided with openings radially distributed. Moreover, the lateral surface is provided with further slots for the outlet of bubbles.
Preferably, the minor base consists of a tapered element with the apex of the cone turned towards the inside of the diffuser.
The distributor is fixed to the cylindrical body by means of another hopper quite similar to the one of the sparger, with the major base facing upwards so that this hopper is capable of helping the discharge of the air-water mixture.
The described diffusers are uniformly distributed at the bottom of the tank and anchored to supports, in the shape of concrete blocks, preferably by means of tie rods fixed with bolts screwed on threaded rods protruding from the concrete blocks, a perforated plate that is inserted on the aforesaid rods being foreseen at the lower end of the tie rod. At the top, the tie rods are fixed on the protruding edge of the second sparger that surrounds the distributor, preferably with nuts screwn on their threaded ends by interposing suitable washers.
The present invention according to a preferred but not limitative embodiment, is shown in the enclosed drawings, in which:
FIG. 1 shows a partially sectioned side view of the diffuser anchored at its support;
FIG. 2 shows a side view of the sparger;
FIG. 3 shows a view of the sparger taken along line 3--3 of FIG. 2;
FIG. 4 shows a view of the sparger taken along line 4--4 of FIG. 2;
FIG. 5 shows a partially sectioned side view of the distributor;
FIG. 6 shows an upper view of the distributor;
FIG. 7 shows a detail of the sparger;
FIG. 8 shows a section of the tank with the diffusers installed.
A diffuser 10 is shown in FIG. 1 comprising a cylindrical body 11 containing two helical sections 12 and 12a that cross each other, forming two spiral canals for discharging the air-water mixture to be treated. The cylindrical body 11 is preferably made of a plurality of sections 11a. The diffuser is provided at its base with a sparger, or dispersing means 13 and at the top with a distributor 14 which is held on the end of the diffuser by means of a second sparger 13a, the hopper 15 of which laterally surrounds said distributor 14.
The sparger 13 (that is quite similar to sparger 13a) is shown in detail in FIGS. 2, 3 and 4. It is made of a hopper 15, the minor base of which has a periphery 17 provided with tongues 16 perpendicular to said periphery 17. The minor base is also provided with a protruding edge 18 having openings 19 for the passage of tie rods 21 (FIG. 1) fixing the diffuser 10. The side surface of the hopper (15) has further openings 20 so as to allow the fixing tie rods 21 to extend perpendicular to support 22 on which they are fixed. This protruding edge 18 also has reinforcements 23 circumferentially disposed.
The minor base of hopper 15 is provided circumferentially with a seat 28 capable of receiving an end of the cylindrical body 11.
Distributor 14 is shown in FIGS. 5 and 6. It comprises a truncated cone shaped portion 24, the minor base of which consists in a tapered element 25 having the apex of the cone turned towards the inside of portion 24. It can be noticed that the tapered element is provided with openings 26, having almost trapezoidal shape. Furthermore, the truncated cone shaped portion 24 is also laterally provided with rectangular openings 27. These openings 26 and 27 are used for the distribution of the mixture of air-water to be treated.
Said truncated cone portion 24 is held at the end of the cylindrical body 11 by means of a second sparger 13a over-turned with respect to the position of sparger 13 (see FIG. 1). An engaging means 29 is foreseen inserted in seat 28 of the minor base of the hopper 15, placed along the major base of the truncated cone portion 24.
A detail of the protruding edge 18 is shown in FIG. 7; the reinforcements 23 and the openings 19 for the passage of tie rods 21 are clearly visible.
FIG. 8 shows a transverse section of a tank used for the aerobic treatment of waste waters; in said tank the diffusers 10 are placed and kept in their position on supports 22 in the shape of concrete blocks. The diffusers are placed on top of conduits 35 for the blown-in air, that run horizontally near the bottom of the tank, these conduits 35 also being anchored to support 22 and provided in the lower part with openings for the air distribution.
FIG. 1 shows a perforated fastening system in detail, however it is obvious that other systems can be used. Tie rods 21 have at the lower end a perforated plate 32 inserted on the threaded rods 30 protruding from support 22, the perforated plate being held in place by a nut 31 and washers. The tie rods are fixed at the top to the protruding edge 18 of the sparger 13a by means of nuts screwed on their threaded ends extending from apertures 19.
The function of the diffuser is as follows: the air bubbles delivered from conduit 35 are caught and divided by means of the lower sparger 13, thus they enter the cylindrical body 11 where they follow a spiral path mixing and interact with the liquid to be treated, finally they reach distributor 14 and exit finely divided.

Claims (12)

I claim:
1. A diffuser (10) comprising a cylindrical body (11) having a base and a top, at least a helical section (12, 12a) inside the cylindrical body, a dispersing means (13) at the base of the cylindrical body and a distributor (14) at the top of the cylindrical body, said dispersing means (13) comprising a frusto-conical skirt (15) having a major base and a minor base, and internal tongues (16) that extend radially from said frusto-conical skirt.
2. A diffuser as in claim 1, further comprising a second dispersing means (13a) at the top of the cylindrical body, around the distributor (14).
3. A diffuser as in claim 1, fixed to a support (22) by means of tie rods (21), said tie rods (21) having a lower end fast with a perforated plate (32) inserted on threaded rods (30) protruding from the support (22), the plate being fixed by means of a nut (31) and washers.
4. A diffuser as in claim 3, wherein the tie rods (21) have an upper end fixed to the protruding edge (18) of the second dispersing means (13a).
5. A diffuser as claimed in claim 1, wherein the minor base of said dispersing means (13) is provided with a protruding edge (18) having openings (19) for the passage of tie rods (21) therethrough to fix the diffuser (10), and said minor base being provided circumferentially with a seat (28) capable of receiving an end of the cylindrical body (11).
6. A diffuser as in claim 5, wherein openings (20) are provided through the frusto-conical skirt (15) of the dispersing means (13).
7. A diffuser as in claim 5, wherein said protruding edge (18) is provided with reinforcements (23).
8. A diffuser as in claim 1, wherein the distributor (14) comprises a frusto-conical portion (24) with an open major base and a minor base provided with radially distributed openings (26), the frusto-conical portion (24) having a lateral surface with additional openings (27) provided therein.
9. A diffuser as in claim 8, wherein the minor base of the frusto-conical portion (24) of the distributor (14) consists of a conical element (25) having an apex thereof directed toward the inside of the distributor (14).
10. A diffuser as in claim 8, wherein the radially distributed openings (26) have a substantially trapezoidal shape.
11. A diffuser as in claim 8, wherein the additional openings (27), provided in the lateral surface of the frusto-conical portion (24), are rectangular.
12. A diffuser as in claim 8, wherein the open major base of the frusto-conical portion of the distributor is provided circumferentially with an engaging means (29) to be inserted in a seat (28) of the second dispersing means.
US07/350,528 1986-11-06 1987-11-04 High yield air diffuser for tanks used in the aerobic treatment of waste waters Expired - Fee Related US5032324A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT23601[U] 1986-11-06
IT2360186U IT209737Z2 (en) 1986-11-06 1986-11-06 HIGH PERFORMANCE AIR DIFFUSER FOR AEROBIC WASTE TREATMENT TANKS.

Publications (1)

Publication Number Publication Date
US5032324A true US5032324A (en) 1991-07-16

Family

ID=11208472

Family Applications (1)

Application Number Title Priority Date Filing Date
US07/350,528 Expired - Fee Related US5032324A (en) 1986-11-06 1987-11-04 High yield air diffuser for tanks used in the aerobic treatment of waste waters

Country Status (8)

Country Link
US (1) US5032324A (en)
EP (1) EP0329703B1 (en)
KR (1) KR890700111A (en)
CN (1) CN1010474B (en)
AU (1) AU607954B2 (en)
CA (1) CA1326718C (en)
IT (1) IT209737Z2 (en)
WO (1) WO1988003514A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2316014A (en) * 1996-08-10 1998-02-18 Robert Howard Smith Water oxygenating cylinder
DE19751884A1 (en) * 1997-11-22 1999-06-02 Jianming Dr Ing Shang Liquid mixer for use in the drinks industry
US20110026255A1 (en) * 2008-01-11 2011-02-03 Kwak Steven E Cable Holding and Positioning Device with Easily Separated and Reconnected Interlocking Components

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19832224C1 (en) * 1998-07-17 2000-02-24 Brochier Wasser Und Abwasserte Height-adjustable water aeration air supply has adjustable clamp facilitating accurate capture of the water bubbles by the funnel, in spite of any slope in the basin floor
US6860473B2 (en) * 2001-02-05 2005-03-01 Masataka Oshima Supporting structure and supporting bracket of single tube drift generator receiving centrifugal force of internal fluid
TWI568685B (en) * 2014-04-21 2017-02-01 Kang Na Hsiung Enterprise Co Ltd Diffuser

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2353195A (en) * 1940-08-03 1944-07-11 Sims Alfred William Mixing fluids of different temperatures and densities
US2967399A (en) * 1957-07-12 1961-01-10 Pneumatic Breakwaters Ltd Artificial breakwaters
US3148509A (en) * 1960-10-24 1964-09-15 Pneumatic Breakwaters Ltd Wave reduction, de-icing and destratification apparatus
US3452966A (en) * 1967-08-24 1969-07-01 Polcon Corp Liquid treatment apparatus and method
US3628775A (en) * 1969-02-14 1971-12-21 Atara Corp Sewage-treating system
US3852384A (en) * 1972-07-21 1974-12-03 Environmental Technology Liquid treatment apparatus
JPS5219462A (en) * 1975-08-06 1977-02-14 Aiko Kojima Waste water treating apparatus (26)
US4051035A (en) * 1976-08-16 1977-09-27 Ralph B. Carter Company Apparatus for the aerobic treatment of liquid waste
GB1519644A (en) * 1976-10-19 1978-08-02 Engineering Technical Services Apparatus for circulating and gasifying a liquid
US4138335A (en) * 1975-04-21 1979-02-06 Atara Corporation Sewage aerating structure
DE2736271A1 (en) * 1977-08-11 1979-02-22 Juergen Ing Grad Krampitz Mixing gas into liquid - using air lift pump principle with venturi throat to induce movement and recycling in liquid esp. for flocculation or froth flotation
FR2528324A1 (en) * 1982-06-14 1983-12-16 Omnium Traitement Valorisation REACTOR FOR THE INJECTION OF GAS IN A LIQUID
DE3241724A1 (en) * 1982-11-11 1984-05-17 Metallgesellschaft Ag, 6000 Frankfurt Device for aerating liquids
US4569757A (en) * 1980-12-10 1986-02-11 Champion International Corporation Adapter skirt for static aerator mixer

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2353195A (en) * 1940-08-03 1944-07-11 Sims Alfred William Mixing fluids of different temperatures and densities
US2967399A (en) * 1957-07-12 1961-01-10 Pneumatic Breakwaters Ltd Artificial breakwaters
US3148509A (en) * 1960-10-24 1964-09-15 Pneumatic Breakwaters Ltd Wave reduction, de-icing and destratification apparatus
US3452966A (en) * 1967-08-24 1969-07-01 Polcon Corp Liquid treatment apparatus and method
US3628775A (en) * 1969-02-14 1971-12-21 Atara Corp Sewage-treating system
US3852384A (en) * 1972-07-21 1974-12-03 Environmental Technology Liquid treatment apparatus
US4138335A (en) * 1975-04-21 1979-02-06 Atara Corporation Sewage aerating structure
JPS5219462A (en) * 1975-08-06 1977-02-14 Aiko Kojima Waste water treating apparatus (26)
US4051035A (en) * 1976-08-16 1977-09-27 Ralph B. Carter Company Apparatus for the aerobic treatment of liquid waste
GB1519644A (en) * 1976-10-19 1978-08-02 Engineering Technical Services Apparatus for circulating and gasifying a liquid
DE2736271A1 (en) * 1977-08-11 1979-02-22 Juergen Ing Grad Krampitz Mixing gas into liquid - using air lift pump principle with venturi throat to induce movement and recycling in liquid esp. for flocculation or froth flotation
US4569757A (en) * 1980-12-10 1986-02-11 Champion International Corporation Adapter skirt for static aerator mixer
FR2528324A1 (en) * 1982-06-14 1983-12-16 Omnium Traitement Valorisation REACTOR FOR THE INJECTION OF GAS IN A LIQUID
US4504388A (en) * 1982-06-14 1985-03-12 Otv (Omnium De Traitement Et De Valorisation) Reactor for injection of gas into a liquid
DE3241724A1 (en) * 1982-11-11 1984-05-17 Metallgesellschaft Ag, 6000 Frankfurt Device for aerating liquids

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
The American College Dictionary, Apr. 1982, p. 1171. *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2316014A (en) * 1996-08-10 1998-02-18 Robert Howard Smith Water oxygenating cylinder
EP0826640A2 (en) * 1996-08-10 1998-03-04 Robert Howard Smith A water oxygenating device
EP0826640A3 (en) * 1996-08-10 1998-04-22 Robert Howard Smith A water oxygenating device
DE19751884A1 (en) * 1997-11-22 1999-06-02 Jianming Dr Ing Shang Liquid mixer for use in the drinks industry
US20110026255A1 (en) * 2008-01-11 2011-02-03 Kwak Steven E Cable Holding and Positioning Device with Easily Separated and Reconnected Interlocking Components
US8313217B2 (en) 2008-01-11 2012-11-20 Kwak Steven E Cable holding and positioning device with easily separated and reconnected interlocking components
US8672511B2 (en) 2008-01-11 2014-03-18 Steven E. Kwak Cable holding and positioning device with easily separated and reconnected interlocking components

Also Published As

Publication number Publication date
IT8623601V0 (en) 1986-11-06
IT209737Z2 (en) 1988-10-24
CN1010474B (en) 1990-11-21
KR890700111A (en) 1989-03-02
WO1988003514A1 (en) 1988-05-19
CN87107373A (en) 1988-05-18
AU607954B2 (en) 1991-03-21
AU8236587A (en) 1988-06-01
EP0329703A1 (en) 1989-08-30
CA1326718C (en) 1994-02-01
EP0329703B1 (en) 1991-06-19

Similar Documents

Publication Publication Date Title
US4650577A (en) Apparatus for treating and purifying waste water
US4863644A (en) Gas diffuser
FI70005C (en) VAETSKEBEHANDLINGSANORDNING
US4210534A (en) Multiple stage jet nozzle and aeration system
US5785854A (en) Current and aeration system for wastewater plant
US4216085A (en) Flotation method and apparatus
US3228526A (en) Apparatus for gasification of liquids
US5490935A (en) Method for treating wastewater
US3206032A (en) Sewage disposal tank
US5032324A (en) High yield air diffuser for tanks used in the aerobic treatment of waste waters
IL44395A (en) Apparatus for aeration and mixing of liquids
US1790975A (en) dallas etal
CA1038090A (en) Reactor for biological water treatment
US4486361A (en) Apparatus for introducing gas into a liquid mass
US6200470B1 (en) Sub-soil domestic wastewater treatment apparatus having multiple aeration chambers
US5954953A (en) Apparatus for treating wastewater
US1937434A (en) Sewage treatment
US3679187A (en) Air diffusion apparatus for the treatment of polluted water
US2172646A (en) Activated sludge apparatus
US4707254A (en) Apparatus for purifying water
US5160610A (en) Radial header for dissolved air flotation systems
US5196114A (en) Aerobic septic system
US6224773B1 (en) Wastewater treatment system with enhanced directional flow
US2082759A (en) Method and apparatus for treatment of sewage
US3239067A (en) Combined clarifier and digester of high capacity

Legal Events

Date Code Title Description
FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: SMALL ENTITY

FPAY Fee payment

Year of fee payment: 4

REMI Maintenance fee reminder mailed
FPAY Fee payment

Year of fee payment: 8

SULP Surcharge for late payment
LAPS Lapse for failure to pay maintenance fees
FP Lapsed due to failure to pay maintenance fee

Effective date: 20030716

STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362